US5102422A - Methods for leather processing including liquid enzyme formulation - Google Patents

Methods for leather processing including liquid enzyme formulation Download PDF

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US5102422A
US5102422A US07/152,020 US15202088A US5102422A US 5102422 A US5102422 A US 5102422A US 15202088 A US15202088 A US 15202088A US 5102422 A US5102422 A US 5102422A
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liquid
enzyme
enzymes
activity
proteases
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Juergen Christner
Ernst Pfleiderer
Tilman Taeger
Ursula Bernschein
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Roehm GmbH Darmstadt
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • CCHEMISTRY; METALLURGY
    • C14SKINS; HIDES; PELTS; LEATHER
    • C14CCHEMICAL TREATMENT OF HIDES, SKINS OR LEATHER, e.g. TANNING, IMPREGNATING, FINISHING; APPARATUS THEREFOR; COMPOSITIONS FOR TANNING
    • C14C1/00Chemical treatment prior to tanning
    • C14C1/06Facilitating unhairing, e.g. by painting, by liming
    • C14C1/065Enzymatic unhairing
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/38Products with no well-defined composition, e.g. natural products
    • C11D3/386Preparations containing enzymes, e.g. protease or amylase
    • C11D3/38663Stabilised liquid enzyme compositions
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/96Stabilising an enzyme by forming an adduct or a composition; Forming enzyme conjugates

Definitions

  • the present invention relates to liquid enzyme preparations comprising an anhydrous organic liquid as a vehicle for an enzyme, suitably together with an additive modifying the rheology of the composition, and to methods for making leather employing such preparation.
  • IE industrial enzymes
  • amylase gamma-aminobutyrotransaminase
  • cellulase collagenase
  • glucose oxidase glutamic acid decarboxylase
  • hemicellulase invertase
  • catalase lipase
  • pectinase penicillase
  • protease and streptokinase, among others.
  • the media in which the enzymes occurring in nature are active are predominantly aqueous media, where a certain dependence on the pH value and on the dissolved constituents of the aqueous medium is frequently observed, and the aqueous medium may therefore be regarded as the standard medium in enzymatic reactions.
  • enzymes are polypeptides whose activity depends primarily on their structural organization and which, like other proteins, can also be denatured by certain organic solvents, caution has always been indicated in the use of organic solvents together with enzymes.
  • liquid preparations In handling chemical agents, and especially in proportioning them, it is often considered an advantage when they are present in liquid form. As a rule, incorporating liquid preparations into liquid reaction media entails fewer problems than admixing powders or other solids. This is true also of enzyme preparations.
  • liquid enzyme preparations in particular pose many problems. The most important of these has to do with the the stability of such enzyme preparations.
  • enzymes in an aqueous medium are subject to the influence of other constituents of the medium, such as acids, bases, salts, surface-active and complexing components, other macromolecules, and particularly other enzymes, the substrates on which the enzymes act, and so forth.
  • Such additives may have either a stabilizing or a destabilizing effect.
  • stabilizing additives for certain enzymes in aqueous solutions glycols, polyglycols, surfactants, proteins and protein hydrolyzates, synthetic polymers, carboxylic acids, specific cations or anions and the like have been proposed, for example.
  • liquid enzyme preparations have failed so far to gain commercial acceptance.
  • liquid enzyme formulations (a) which are stable under the conditions of use, (b) in which the activity of the enzymes preferably is not affected or not irreversibly affected, (c) which are compatible with the intended end-use areas of the enzymes, and (d) which are economically and ecologically acceptable.
  • the loss of activity of such a so-called liquid enzyme should not exceed 15 percent over a period of from four to six months.
  • the invention relates to liquid enzyme formulations for technical use wherein the vehicle for the enzymes is at least one substantially anhydrous organic liquid or a mixture of such liquids.
  • Suitable liquids for this purpose are liquids which are consonant with the above requirements, are advantageously in common use, and preferably are ecologically safe and in particular substantially nontoxic and noninjurious to enzymes.
  • the organic liquids to be used in accordance with the invention are preferably hydrocarbons, but may contain oxygen or, less preferably, sulfur. Liquids of the formula (I)
  • R 1 and R 2 are preferred, wherein, when X is carbonyl, R 1 and R 2 are the same or different alkyl having 1 to 3 carbon atoms. If X is COO, then R 1 and R 2 are the same or different alkyl having 1 to 6 carbon atoms or R 1 is hydrogen and R 2 is such alkyl. If X is oxygen or sulfur, R 2 is hydrogen or alkyl having 1 to 8 carbon atoms and R 1 may be alkyl having 1 to 8 carbon atoms, or is ##STR1## in which R 3 is hydrogen, --CH 3 or --CH 2 OH, or R 1 is --(CH 2 --CH 2 O) n --H, where n is an integer from 1 to 15.
  • R 1 and R 2 may also each be --CH 2 --CH 2 OH.
  • R 1 and R 2 taken together with an oxygen or sulfur atom therebetween, may form a 5- or 6- membered ring in which all ring members are --CH 2 --, except that one such ring member may be carbonyl (C ⁇ O) and one further such ring member may be oxygen.
  • Additional liquids include those of the formula (II) ##STR2## wherein R 5 is --CH 3 or --CH ⁇ CH 2 .
  • liquids of formula (I) are particularly carbonic esters, and more particularly cyclic carbonic esters such as ethylene carbonate and, specifically, propylene carbonate.
  • polyhydric alcohols such as glycerol, ethylene glycol, butyl glycol, butyl diglycol, diethylene glycol, polyethylene glycols (MW at least 400), liquid polypropylene glycols, and etherified derivatives thereof; monovalent alcohols or fatty alcohols such as methanol, ethanol, isopropanol, n-butanol, isobutanol, 2-ethyl hexanol, and cyclohexanol; ethers such as diethylether, methoxypropanol, diethylene glycol monomethyl ether, and particularly cyclic ethers such as dioxan and tetrahydrofuran; ketones such as acetone, ethylmethyl ketone, and cyclohexanone; esters such as acetone
  • oxoalcohols and their ethoxylation products having 3 to about 14 ethylene oxide units
  • fatty alcohols and their ethoxylation products olefins and their sulfonated derivatives such as C 9 -C 12 -a-olefin sulfonate, for example in the form of the sodium salt
  • fatty alcohol ether sulfates such as sulfated C 12 -C 15 -alcohols, condensed with ethylene oxide.
  • fatty acid alkanolamides such as C 16 -C 18 -fatty acid ethanolamide
  • alkylphenol compounds such as octylphenol and ethoxylated derivatives thereof, such as nonylphenol ethoxylate with 8-9 moles of ethylene oxide.
  • mixtures of organic liquids can be of advantage.
  • liquids of formula II are toluene and styrene.
  • turpentine, solvent naphtha, white spirit, aliphatic hydrocarbons, and petroleum oils are useful.
  • solvent naphtha preferably between 50° C. and 180° C., and especially between 70° C. and 150° C.
  • polyethylene glycols as a rule these are liquids having a molecular weight less than 110 and for the most part having a boiling point below 300° C. at normal pressure.
  • the organic liquids to be used according to the invention are essentially anhydrous, i.e. as a rule they contain less than 1 percent by weight of water, and preferably not more than the usual mechanically held moisture. Drying of the liquids is carried out conventionally, for example by means of commonly used desiccants distillation, including azeotropic distillation, etc. (See Houben-Weyl, vol. I/2, pp. 765-886, Georg Thieme Verlag, 1959).
  • the enzyme formulations may further contain surfactants.
  • Preferred are nonionic surfactants of the type of the fatty alcohol/alkyl phenol ethoxylates (with oleocetyl-and olein-alcohol, for example); moreover, adducts of polyglycols with from 4 to 42 moles of ethylene oxide, apart from anionic types such as alkyl sulfates, alkyl ether sulfates, alkyl phosphates, alkyl ether phosphates, alkyl sulfonates and alkylaryl sulfonates.
  • the amount of the surfactants generally ranges from 0.001 to 50 weight percent, and preferably from 0.005 to 20 weight percent, based on the liquid vehicle.
  • the hydrophile-lipophile balance (HLB) of the emulsifiers (or the o/w emulsifying action) generally ranges from 8 to 18, and preferably from 9 to 15.
  • HLB hydrophile-lipophile balance
  • Also preferred are liquids which do mix with water, and especially liquids which are miscible with water in any ratio. On first approximation, it should be assumed that the enzymes remain completely undissolved in the liquids. The tendency to self-digestion or to decomposition of other enzymes thus is greatly minimized.
  • the quantity of the liquids used is based mainly on practicality in the handling of the enzymes and is not really critical.
  • the weight ratio of enzyme to liquid will not be less than 1:10, for reasons of handling ease.
  • the upper limit of the weight ratio of enzyme to liquid will generally range from 1:30 to 1:500.
  • a ratio of enzyme to liquid of from 1 to about 50 has proved practical.
  • mixtures of the liquids recited above may be used.
  • the enzymes which are essentially proteins, are added to the substantially anhydrous liquids, problems such as slow wetting and/or dispersal problems such as settling or creaming may arise.
  • silicon dioxide The pyrogenic modifications of silicon dioxide are known to be prepared by gas-phase reactions, for example by flame hydrolysis or by use of an electric arc. They generally consist of spherical particles having a primary particle size from 5 to 500 nanometers. Their density is about 2.2 g/cm 3 . Such materials are available commercially under the names "Aerosil” and "Cab-o-Sil".
  • clays particularly bentonite
  • pectinases are adsorbed on bentonite with loss of activity.
  • Kaolin and bentonite are known to form thixotropic gels with a number of polar and nonpolar organic liquids.
  • the thixotropy of the gels disappears upon the addition of minor amounts of longer-chain alcohols, for example.
  • clays are meant the usual aluminosilicates, and by bentonites the commercial preparations consisting mainly of montmorillonite (Al 2 O 3 ⁇ 4SiO 2 ⁇ H 2 O).
  • montmorillonite Al 2 O 3 ⁇ 4SiO 2 ⁇ H 2 O
  • organically activated bentonites for example, those formed by reaction of sodium montmorillonite with quaternary alkylammonium compounds. Through cation exchange, so-called organophilic bentonites, which swell in organic liquids, are formed.
  • organophilic bentonites which swell in organic liquids, are formed.
  • the commercial grades flakes, particle sizes ranging from 0.5 to 5 microns
  • the liquids should contain from 0.1 to 3 weight percent, and preferably from 0.3 to 1 weight percent, based on the liquid , of inorganic additives. It has proved particularly advantageous to subject the inorganic addition to the enzyme concentrate, together with the liquid, to shearing action in appropriate equipment, and particularly in a dispersion mill.
  • the latter may be of the commercial type. (See Ullmanns Enzyklopadie der ischen Chemie, 4th ed., vol. 1, p. 239, Verlag Chemie, 1972.)
  • the rotational speed and the treating time depend mainly on the type of the equipment.
  • a treating time of from 2 to 60 minutes at a peripheral speed of from 4 to 36 meters per second will serve as a guide for the action of commercial dispersing apparatus on bentonite in one of the liquids to be used in accordance with the invention.
  • Propylene carbonate has been found to be a particularly effective liquid, especially in combination with silicon dioxide or with bentonite.
  • the formulations of the invention are not subject to any restrictions with respect to the enzyme component, except insofar as the stability of the enzymes themselves to organic liquids such as alcohols is concerned.
  • a requirement is that the organic liquid vehicle must be compatible with the end use of the enzymes. It was not to be foreseen that, by the use of inorganic dispersing agents, organic liquid carrier systems for enzymes could be prepared, which systems would in general more closely approach the ideal requirements of technology, not only from the viewpoint of physical and biological stability, but also from the point of view of ready availability.
  • the vehicle contains from 1 to 10 percent by weight of hydrocarbons, and particularly branched or linear aliphatics having from 5 to 20 carbon atoms.
  • hydrocarbons and particularly branched or linear aliphatics having from 5 to 20 carbon atoms.
  • branched or linear aliphatics having from 5 to 20 carbon atoms.
  • Illustrative of these are petroleum fractions in the boiling range of approximately 50° to 180° C. See also the above definition of liquid.
  • the enzymes are primarily those which are already being used industrially or in other fields of application. (See “The Prior Art” above.)
  • Pancreatin, and particularly trypsin and chymotrypsin (optimum pH range about 7 to 10);
  • Pepsin (EC 3.4.23.1) (optimum pH range about 1.5 to 4.0;
  • Cathepsin (EC 3.4.23.5) (optimum pH range about 4.0 to 5.0).
  • bacillus species for example, B. subtilis, B. licheniformis, B. alkalophilus, B. cereus, B. natto, B. vulgatus, B. mycoides.
  • streptomyces for example, Streptomyces fradiae, S. griseus, S. rectus.
  • Enzymes are classified not only according to their source but also on the basis of the site of attack (exoenzymes vs. endoenzymes) and of the active site of the proteases (serine proteases, which are inhibited by diisopropyl fluorophosphate [DFP]; sulfhydril enzymes).
  • enzyme activity is a function of pH.
  • proteases are therefore classed as follows:
  • Neutral proteases with optimum activity in the pH range from 6.0 to 9.0 and particularly neutral bacterial proteases (EC 3.4.24), which belong to the metalloenzymes, and fungal proteases such as bacillus proteases, pseudomonas proteases, streptomyces proteases, and aspergillus proteases.
  • Proteases are used industrially in leather manufacture, in detergents and in cleansing, in desizing, in cheesemaking, in the tenderization of meats and in the stabilization of beer, for example.
  • alkaline proteases are, in particular, the subtilisins, alkaline bacterial proteinases of the serine type, which in the pH range from 9 to 10 are stable and relatively insensitive to perborate.
  • the proteolytic activity of enzymes is usually determined by the Anson hemoglobin method (M. L. Anson, J. Gen. Physiol. 22, 79 [1939 or by the Lohlein-Volhard method ("Die Lohlein-Volhard'sche Methode Kunststoff Beêt der proteolytician Aktivitat" in Gerschenbuch, Dresden/Leipzig, 1955) and in that case expressed in LVU (Lohlein-Volhard units).
  • An LVU is the amount of enzyme which under the specific conditions of the method digests 1.725 mg of casein.
  • units are also used in what follows which are derived from the Anson method. These units are known as "proteinase units (hemoglobin)", or U Hb .
  • U Hb proteinase units
  • alpha-Amylases alpha-1,4-glucosan hydrolases (EC 3.2.1.1)
  • Exoamylases sacharogenic amylases
  • beta-Amylases alpha-1,4-glucosanmaltohydrolases (EC 3.2.1.2)
  • Alpha-amylases are known to occur in plants, for example, together with beta-amylases. They are commercially produced from pancreas and from bacterial and fungal cultures.
  • bacillus species such as B. subtilis, B. mesentericus, B. polymixa, B. amyloliquefaciens and B. licheniformis; from fungi, and particularly from aspergillus species such as A. niger, A. phoenicis, A. oryzae and A. awamori; from Mucor strains such as M. rouxianus; from Rhizopus strains such as R. delemar, R. oryzae and R. japonicus; and from endomyces strains such as E. fibuliger.
  • the pH optimum of alphaamylases is predominantly in the range from 4.7 to 7.2.
  • Amylases find use in the food industry (see “Biotechnology” H.-J. Rehm & G. Reed, ed. , vol. 5, Verlag Chemie, 1983; “Industrial Aspects of Biochemistry”[B. Spencer, ed.], vol. 30, part I, pp. 139-186 and 213-260, Elsevier [1973]), in the liquefaction of starch, in malt production, in the production of ethanol, in desizing, in leather manufacture, etc.
  • alpha-amylases can be determined, when starch is used as the substrate, by the method of Sandstedt, Kneen & Blish (Cereal Chem. 16, 172 [1939] and Technical Bulletin No. 1024, U. S. Department of Agriculture).
  • the Willstatter method is used to determine the activity of pancreatic amylase. (Hoppe-Seylers, Z. physiol. Chem. 126, 143 [1923].)
  • a Willstatter amylase unit is defined as 100 times the amount of enzyme which under the test conditions specified breaks down starch at such a rate that the monomolecular reaction constant is 0.01.
  • lipases are carboxyl esterases which cleave glycerol ester in aqueous emulsion. Thus they differ from other carboxyl esterases which attack the substrate in aqueous solution.
  • the pancreatic enzyme complex contains, apart from lipases, mostly esterases as well as proteases and amylases as commercially important companion enzymes.
  • the pH optimum (for olive oil) is in the range from 7 to 8.5, with the range of activity extending from pH 6.5 to 9.5.
  • Lipases are generally highly-unstable, especially to proteolytic breakdown by companion proteases.
  • Microbiological lipases for example, from Pseudcmonas fragii, Aspergillus species (e.g., A. luchuensis, Candida cylindracea, Geotrichum candidum, Humicola lanuginosa, Mucor pusillum, Penicillium species (e.g., P. chrysogenum, P. oxalicum), and Rhizopus species (R. nigricans, R. oryzea).
  • Pseudcmonas fragii Aspergillus species
  • Aspergillus species e.g., A. luchuensis, Candida cylindracea, Geotrichum candidum, Humicola lanuginosa, Mucor pusillum, Penicillium species (e.g., P. chrysogenum, P. oxalicum), and Rhizopus species (R. nigricans, R. oryzea).
  • lipases generally have at least one pH optimum at a pH above 7.0. To the extent that their instability permits it, lipases find use in waste disposal, in leather manufacture and in the food industry, for example.
  • microorganisms for example, from Micrococcus lysodeicticus.
  • Catalases are used in peroxide bleaching and in the milk industry.
  • cellulase is an enzyme complex whose components successively take part in the breakdown of native cellulose.
  • Cellulases are found in insects, mollusks and microorganisms (bacteria, mold fungi). Commercially utilized sources of cellulases are particularly aspergillus, neurospora, rhizopus, trichoderma and trametes strains.
  • Enzyme preparations are further used to dissolve untanned machine trimmings and other byproducts of leather manufacture (U.S. Pat. No. 4,210,721, Swiss patent 631,486, U.S. Pat. Nos. 4,293,647 and 4,220,723), keratin-containing raw stock (U.S. Pat. No. 4,232,123), elastin-containing preparations (U.S. Pat. No. 4,179,333); for working up collagen-containing raw stock (U.S. Pat. No. 4,220,714), etc.
  • liquid enzyme formulations in accordance with the present claims may be used in the various operations of leather manufacture (see Ullmanns Enzyklopadie der ischen Chemie, 3rd ed., vol. 11, p. 609, Urban/Schwarzenberg; Ullmanns Enzyklopadie der ischen Chemie, 4th ed., vol. 16, pp. 111-174, Verlag Chemie, 1978; F. Stather, Gerschenemie und Gerbereitechnologie, 4th ed., Akademie-Verlag, Berlin, 1967), namely:
  • the soaking of hide stock, in which the hardening of the, hides, or skins, resulting from salt curing is reversed, is usually carried out at a pH between 7.0 and 10.0.
  • the concurrent use of enzymes, and particularly of proteolytic enzymes accelerates the softening action through "digestion” of the water-soluble and other albumins which are not a part of the collagenous fiber structure of the hide.
  • enzymes whose range of activity (or pH optimum of the proteolytic activity) falls between pH 7.00 and 10.0 are employed in soaking. Removal of the noncollagenous albumins assures faster and more intensive wetting of the hide.
  • the soak water is advantageously made slightly alkaline; however, the pH value should always remain below 12.
  • soaking aids such as monoethanolamine with an antiseptic such as zephyrol or naphthalenesulfonic acid in combination with substituted phenols; highly sulfonated ricinoleic acid butyl ester with a methylcyclohexanol mixture fatty alkyl sulfates with solvents.
  • suitable enzymatic additives for the inventive liquid enzyme formulations are the proteases listed under (A) above, and particularly those named under (A) (c), and more particularly microbial proteases active in the pH range from 4 to 9.5, especially fungal proteinases from aspergillus species such as A. saitoi and A. usamii, for example, and particularly acid proteinases with activity in the pH range from 2.5 to 4.5; also those from A. oryzae active in the pH range from 4.0 to 9.5, and those from A. niger and A. flavus active in the pH range from 9.5 to 11.0.
  • the concentration of proteolytic activities of the proteinases used generally ranges from 0.1 to 1.0 Anson units, or from 1,000 to 3,000 LVU, per liter of soak liquor.
  • the soak liquors may, further contain amylases according to (B) above.
  • Amylases occur as companion enzymes of fungal proteinases. They promote the cleavage of glucosidic bonds in the proteoglycans and glycoproteins of the hide.
  • amylases of microbial origin and more particularly those from aspergillus species such as A. oryzae and A. niger, especially those active in the pH range from 3.0 to 5.8. Suited for use are also those of bacterial origin, for example, those derived from Bacillus subtilis, B. mesentericus and B. polymixa with activity in the pH range from 5.0 to 7.0.
  • the glycolytic activity of amylases ranges from 500 to 2,000 SKB.
  • the temperature of the soak liquors is advantageously higher than 20° C.
  • the soaking duration should be as short as possible and generally is between 4 and 36 hours.
  • lime liquors are used most often.
  • sharpened lime liquors preferably a combination of calcium hydroxide and sodium sulfide
  • swelling-inhibiting liming aids such as wetting agents, and particularly cationic wetting agents, in combination with monoethanolamine and disinfectants, for example, quaternary alkyldimethylbenzylammonium compounds, or dialkylamine and its sulfate.
  • enzymes which in this pH range remain sufficiently stable may be used in addition to the usual liming chemicals. Soaking and liming may be combined by gradually increasing the pH value and using appropriate enzymes.
  • the hide, freed of curing salt may first be pretreated in the acid pH range with substances cleaving disulfide bridges, and then hair loosening and opening up may be brought about simultaneously without prior soaking by the use of proteases active in the alkaline range at a pH of about 11 to 13. This is then followed by the further processing steps (III) and optionally (IV) usually carried out in the beamhouse. It is advisable to use in the beamhouse operations (II) alkaline bacterial proteinases (serine proteases), for example, from B. subtilis. B. licheniformis, B. firmus, B. alcalophilus, B. polymixa and B. mesentericus.
  • alkaline bacterial proteinases serine proteases
  • proteases generally have an activity ranging from 8,000 to 10,000 LVU per gram. They are advantageously used in amounts of from 0.1 to 10 weight percent, and preferably from 1 to 5 weight percent, based on the weight of the salted hides and skins (raw weight).
  • the enzymatic reaction in unhairing and opening up is carried out at about 18 to 28° C.
  • the reaction time generally ranges from 12 to 24 hours, and more particularly from 12 to 16 hours.
  • Unhairing or dewooling can also be performed with alkaline fungal proteinases of the above type (i), for example, with aspergillus proteases, and particularly with those from A. niger and A. flavus which are active in the pH 9.5 to 11.0 range.
  • alkaline fungal proteinases of the above type (i) for example, with aspergillus proteases, and particularly with those from A. niger and A. flavus which are active in the pH 9.5 to 11.0 range.
  • the enzymatic unhairing method of German patent 34 29 047 in which hides and skins are treated in a liquor in the pH range from 9 to 11 with proteolytic enzymes having optimum activity in the pH range from 2 to 7.5, may be employed, unhairing being then carried out.
  • the enzymes used then are proteases of the above type (iii), and particularly from A. oryzea, A. saitoi, A. parasiticus, A. usamii and A. awamori, from Paelomyces species, Penicillium species or also Rhizopus species and/or from Mucor pusillus as well as the acid proteases listed under (A) (a) and (A) (b) above.
  • the activity generally ranges from 50 to 200 mU Hb .
  • Deliming and bating are preferably carried out with the aid of enzymes.
  • Deliming serves to reduce the alkalinity of the pelts from a pH value between 13 and 14 to a pH of from 7 to 8.
  • Deliming is preferably done, not with strongly dissociated but with weak organic acids of the type of the dicarboxylic acids, Or then with weakly acid salts.
  • residues of epidermis, hair and pigments should be removed and further opening up should be brought about.
  • noncollagenous albumin constituents should be removed. (See Ullmanns, 4th ed., vol. 16, loc. cit., pp. 119-120.)
  • Bating is carried out conventionally at pH 7.5 to 8.5.
  • the use of cyclic carbonates in deliming is known from German patent 31 08 428.
  • the duration of the bate as a rule is between 1 and 6 hours, preferably 1-2 hours as a short bate.
  • the proteases can be used in such amount that from 1 to 10 Lohlein-Volhard units are present per gram of pelt weight.
  • the temperature is advantageously between 25° C. and 35° C., preferably 30° C.
  • Any conventional commercial tanning vessel such as a drum, paddle-vat, mixer, or tanning machine can be used (See O'Flaherty et al., The Chemistry and Technology of Leather, vol. 1, ACS Monograph Series, Reinhold Publishing Corporation, New York 1956).
  • Lipases according to (C) above for example, pancreatic lipases exhibiting activity in the pH 7.0 to 9.0 range, may be used concurrently in bating.
  • Amylases according to (B) above for example, pancreatic amylases which are active at a pH of from 5.5 to 8.5 and promote the cleavage of glycoside linkages in bating, will also exert a beneficial influence on bating, particularly as companion enzymes of trypsin and chymotrypsin.
  • the pelt for mineral tanning has to be acidified, that is, its pH has to be reduced from about 8 to the 3 to 4 range. This is done in the pickle liquor, which is an acid/salt solution in water, for example, sulfuric acid or formic acid together with sodium chloride.
  • mold tryptases for example, optionally together with carbohydrate-splitting enzymes, derived in particular from bacteria or from mold fungi.
  • inventive liquid enzyme formulations offer a generally applicable solution, not likely to give rise to difficulties, to the problem of making use of liquid enzyme formulations, which is often desirable. Being able to combine enzymes with other components which in an aqueous medium and on prolonged exposure would interfere with enzyme activity is a further advantage. This is true particularly of the ability to combine different enzymes, for example, proteases, not only with amylases, lipases, etc., but also with hydrotropes such as urea, guanidine salts, cumene sulfonate, etc.
  • water soluble salts such as ammonium sulfate or sodium sulfate which are commonly added to powdered enzymes as diluents and/or stabilizers can be dispensed with in the preparations of the invention.
  • Nonliquid components amount to only a fraction of those present in conventional preparations.
  • the salt content of prior art products is responsible for a number of leather imperfections which, thus, can be avoided using the new preparations.
  • the invention permits the combination of enzymes with one another, with further treating agents, with activators, and the like, which are incompatible in aqueous concentrates.
  • the enzyme concentration in the preparations of the invention can extend over a wide range.
  • the preparations of the invention are very stable. For instance, a combination of fungus proteases and pancreatic enzymes is still stable after 6 months' storage. The danger of contamination, for instance with microorganisms, is minimized. The need for anti-fungal or anti-bacterial protection is unnecessary. In aqueous liquid enzyme preparations, the stabilizing agents which are employed adversely affect enzyme activity.
  • Uniform enzyme activity experience, especially in the area of conventional leather preparation, has shown that the use of enzymes leads to defects in the product if the enzyme activity is non-uniform, as, for example, in the use of solid enzyme preparations.
  • the liquid preparations of the invention can be dispersed more uniformly and more rapidly.
  • auxiliaries desired in the final product such as builders, polyphosphates, or zeolites, can be dispersed in the liquid organic carrier together with the enzyme, which is not possible using an aqueous phase.
  • Stability to creaming and settling in contrast to enzyme preparations in which, for example, a crystalline enzyme is preserved in an organic liquid such as toluene, whereby the enzyme, for example a pancreatic enzyme, usually settles on the floor of the container, the invention makes available stable enzyme dispersions in which the stabilizer in no way adversely affects the enzyme activity.
  • a fungal protease concentrate derived from Aspergillus parasiticus (150,000 LVU; pH optimum, 7.5 to 9) and 1.48 g of a pancreatic enzyme preparation (220,000 LVU; pH optimum, 6 to 8) are added. Dispersing is then continued at constant rotative speed, care being taken to not exceed a temperature of 40° C.
  • the end product has an activity of 1,000 LVU and exhibits no loss of activity after 4 weeks at 20° C. No creaming or settling of the enzyme is observed in the product.
  • the dispersing conditions (rotative speed) and the type of the organically modified bentonite have to be adjusted according to the type of the solvent, the particle size, and the concentration of the enzyme concentrate.
  • the dispersion is allowed to stand for 24 hours. Under the above dispersing conditions, 18.5 g of a neutral protease from a Bacillus subtilis strain (70,000 LVU/g; pH optimum, 5.5 to 7) is added. Dispersing is continued for another 5 minutes. The end product has an activity of 1,300 LVU. After 5 weeks, no loss of activity is evident from the LVU measurement.
  • the liquid enzyme formulation remains homogeneous; there is no settling or creaming.
  • the hides After a soaking time of 5 hours, the hides have been completely soaked back and are at the same time ready for hair loosening. A large portion of the natural fat in the hides is emulsified in the soak liquor.
  • the hides soaked in the above manner are limed by prior-art methods and processed further into crust leather for shoes.
  • 1,000 g of petroleum, boiling point 110° to 130° C., is heated to 40° C. and after the addition of an organically modified bentonite (e.g., "MPA-X-2000" of Kronos Titan, Leverkusen) dispersed for 10 minutes. Then 2.5 g of an acid fungal protease from Aspergillus parasiticus (80,000 LVU/g; pH optimum, 3.5 to 5) are added and dispersing is continued for another 5 minutes.
  • an organically modified bentonite e.g., "MPA-X-2000" of Kronos Titan, Leverkusen
  • a liquid enzyme formulation having an activity of 200 LVU is obtained which after 4 weeks at 20° C. exhibits no loss of activity.
  • the solution is homogeneous and neither creams nor settles.
  • the pelts are well degreased and loosened due to the action of the enzyme/surfactant/petroleum combination.
  • depickling tanning agents may be added to a replenished or fresh liquor and the stock may then be processed further conventionally.
  • a non-ionic anhydrous wetting agent prepared from nonyl phenol plus 8.5 mol of ethylene oxide and 12 g of fumed silica (Aerosil 380® product of Degussa, Hanau, West Germany) are mixed together with 5 g of a surface active agent (Borchigen STL®, based on modified fatty acid, product of Borchers GmbH, Goslar, W.-Germany) in a stirring vessel.
  • the mixture is dispersed for 15 minutes with a toothed-disk agitator at a rotative speed of 15-18 m/sec.
  • Liquid, biodegradable heavy-duty detergent 466 g of 1,2-propylene glycol * and 400 g of nonionic surfactant (Marlipal® 013-90, isotridecyl alkohol plus 9 moles of ethylene oxide, product of Chemische Werke Huls AG, W.-Germany), 100 g of ethyl alcohol (98%) plus 10 g of fumed silica (Aerosil 380®, product of Degussa AG, W.-Germany) and 4 g of a surface active agent (modified and etherified fatty acid Borchigen STL®,product of Borchers GmbH, Goslar, W.-Germany) are mixed and dispersed in a stirring vessel using a toothed disk agitator for 15 minutes at a rotative speed of 15-18 m/sec. The viscosity of the liquid was found to be 1 250 mPas. The following components are added and are actively dispersed in the order
  • Liquid enzyme composition for the soaking of hides and skins
  • ethylene carbonate 300 g of methyl ethylketone and 264 of nonionic surfactant (C 16 -C 18 fatty alcohol condensed with 9 moles ethylene oxide) are mixed and warmed to 40° C. in a stirring vessel. Then 10 g of fumed silica (Aerosil 380®) and 6 g of Borchigen STL® (see example Q) are added. The mixture is dispersed by means of a toothed-disk agitator at 15-18 m/sec for 15 minutes. The viscosity rises from 60 mPas to 1040 mPas.
  • nonionic surfactant C 16 -C 18 fatty alcohol condensed with 9 moles ethylene oxide
  • pancreatic enzyme concentrate activity 40 000 LVE/g
  • pancreatic enzyme concentrate activity 40 000 LVE/g
  • Activity after this period was found to be 760 LVE (Original activity was 800 LVE/g).

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  • Cosmetics (AREA)
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5531795A (en) * 1992-12-10 1996-07-02 Novo Nordisk A/S Method for casein finishing of leather
US5710040A (en) * 1995-02-24 1998-01-20 Roehm Gmbh Chemische Fabrik Stable enzymatic aqueous liquid composition for the production of leather
US20040006825A1 (en) * 2002-07-15 2004-01-15 Chellan Rose Process for lime and sulfide free unhairing of skins or hides using animal and/or plant enzymes
US20040118360A1 (en) * 2002-12-20 2004-06-24 Visional International, L.L.C. Bleached expanded pigskin and products
US20050071927A1 (en) * 2002-12-20 2005-04-07 Vision International, L.L.C. Bleached expanded pigskin and products
US20060101584A1 (en) * 2002-08-14 2006-05-18 Basf Aktiengesellschaft Formulation for use in chrome or chrome-free tannage
US20120097889A1 (en) * 2010-10-26 2012-04-26 Novozymes Biologicals, Inc. Wastewater Treatment Compositions
US20120142073A1 (en) * 2010-08-05 2012-06-07 West Bengal University Of Technology Hide processing methods and compositions
US20160186275A1 (en) * 2014-12-22 2016-06-30 Zhuangdou Zhang Tanning Process With Reduced Waste Discharge
RU2588984C2 (ru) * 2014-07-04 2016-07-10 Михаил Вячеславович Новиков Способ выделки меховых шкурок
US10501336B2 (en) 2013-12-04 2019-12-10 Zhuangdou Zhang Tannery process with effluent recycling

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5273898A (en) * 1986-10-17 1993-12-28 Noro Nordisk A/S Thermally stable and positionally non-specific lipase isolated from Candida
DE3922748B4 (de) * 1989-07-11 2006-01-05 Röhm GmbH & Co. KG Enzymatisches Weichverfahren
DE3927286C2 (de) * 1989-08-18 1997-07-24 Roehm Gmbh Wäßrige Enzym-Flüssigformulierungen
DE4023601A1 (de) * 1990-07-25 1992-01-30 Henkel Kgaa Fluessige enzymzubereitung
US5320959A (en) * 1990-08-15 1994-06-14 Rhone-Poulenc Inc. Liquid lipase from animal origin and method of preparation
EP0495257B1 (en) * 1991-01-16 2002-06-12 The Procter & Gamble Company Compact detergent compositions with high activity cellulase
US5443750A (en) * 1991-01-16 1995-08-22 The Procter & Gamble Company Detergent compositions with high activity cellulase and softening clays
CZ285164B6 (cs) * 1991-03-26 1999-05-12 Röhm Gmbh Způsob výroby holin, připravených k vyčinění
US5525509A (en) * 1991-03-26 1996-06-11 Rohm Gmbh Method for the enzymatic liming of skins and hides
EP0540784B1 (en) * 1991-11-06 2000-01-19 The Procter & Gamble Company Dye transfer inhibiting compositions
GB9309243D0 (en) * 1993-05-05 1993-06-16 Allied Colloids Ltd Enzyme dispersions,their production and compositions containing them
US5587108A (en) * 1994-10-06 1996-12-24 European Touch Co., Inc. Styrene monomer based nail tip blender and brush cleaner
BR9509246A (pt) * 1994-10-07 1997-10-21 Novo Nordisk As Processo para processamento de peles ou couros de animais em artigos de couro e macerador
JP3625503B2 (ja) 1994-11-11 2005-03-02 旭化成ファーマ株式会社 臨床検査用複合酵素含有組成物
AU3924195A (en) * 1994-11-28 1996-06-19 Novo Nordisk A/S Enzymatic degreasing of skins and hides
US5531898A (en) * 1995-04-06 1996-07-02 International Organic Solutions Corp. Sewage and contamination remediation and materials for effecting same
AU2635097A (en) 1996-04-29 1997-11-19 Novo Nordisk A/S Non-aqueous, liquid, enzyme-containing compositions
US6121041A (en) 1996-07-31 2000-09-19 St. Jude Medical, Inc. Use of microorganisms for decellularizing bioprosthetic tissue
US7001724B1 (en) * 2000-11-28 2006-02-21 Applera Corporation Compositions, methods, and kits for isolating nucleic acids using surfactants and proteases
AU2002366266A1 (en) * 2001-12-19 2003-06-30 Dsm N.V. Method for the inactivation of amylase in the presence of protease
DE10221152B4 (de) * 2002-05-13 2008-10-30 Schill + Seilacher Ag Verfahren zur Herstellung sauberer Blößen in der Wasserwerkstatt
GB2393185B (en) * 2002-09-17 2005-10-12 Generics A novel process for the preparation of 3,3'-azo-bis(6-hydroxybenzoic acid) and its derivatives
BRPI0414417B1 (pt) 2003-12-17 2014-11-25 Akzo Nobel Nv "processo para desengordurar e/ou secar peles de animais".
US7416869B2 (en) * 2004-08-19 2008-08-26 Lonza Ltd. Enzyme delivery systems, application in water based products
WO2008021987A2 (en) * 2006-08-10 2008-02-21 Jon Barron Proteolytic enzyme formulations
CN103046383B (zh) * 2012-11-27 2016-05-04 江南大学 一种酶氧一浴棉型织物低温前处理方法
CN114806737B (zh) * 2022-04-28 2023-09-15 应急管理部天津消防研究所 一种灭火防护服装PAHs污染专用清洁剂及其制备方法和应用

Citations (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE200519C (fi) * 1907-06-06
DE288095C (de) * 1914-11-11 1915-10-18 Roehm Otto Verfahren zum Weichen von Häuten und Fellen
DE847947C (de) * 1943-09-11 1952-08-28 Roehm & Haas G M B H Beizverfahren fuer Pelzfelle
DE927464C (de) * 1953-09-04 1955-05-09 Roehm & Haas G M B H Verfahren zur Herstellung gerbfertiger Bloessen
DE941811C (de) * 1954-11-18 1956-04-19 Roehm & Haas G M B H Verfahren zur Herstellung gerbfertiger Bloessen
DE941680C (de) * 1954-04-17 1956-04-19 Roehm & Haas G M B H Verfahren zur Vorbehandlung von geweichten Pelzfellen fuer die Gerbung
DE1022748B (de) * 1955-11-30 1958-01-16 Roehm & Haas Gmbh Weichen von Fellen und Haeuten
DE1023183B (de) * 1954-06-30 1958-01-23 Roehm & Haas Gmbh Verfahren zum AEschern von Fellen und Haeuten mit Hilfe von Schimmelpilztryptase
DE1026038B (de) * 1955-03-30 1958-03-13 Roehm & Haas Gmbh Enthaaren und Entwollen gruener oder geweichter Felle
DE1034317B (de) * 1955-05-27 1958-07-17 Roehm & Haas Gmbh Verfahren zum Weichen von Rohhaeuten und -fellen
DE974813C (de) * 1954-12-24 1961-05-04 Roehm & Haas G M B H Verfahren zum Beizen tierischer Hautbloessen
DE975095C (de) * 1955-01-01 1961-08-10 Roehm & Haas G M B H Verfahren zum Beizen tierischer Bloessen mit Pankreasenzympraeparaten
DE1120066B (de) * 1955-03-23 1961-12-21 Roehm & Haas Gmbh Verfahren zum Beizen tierischer Hautbloessen
DE1134474B (de) * 1955-03-30 1962-08-09 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE976107C (de) * 1954-05-19 1963-02-28 Roehm & Haas G M B H Verfahren zum Beizen tierischer Hautbloessen fuer Chevreauleder
DE1155560B (de) * 1960-06-04 1963-10-10 Roehm & Haas Gmbh Enthaaren von Haeuten und Fellen mit Hilfe proteolytischer Enzyme
DE976602C (de) * 1954-02-16 1964-01-02 Roehm & Haas G M B H Weichverfahren fuer rohe tierische Felle und Haeute
DE976928C (de) * 1955-01-08 1964-08-20 Roehm & Haas G M B H Verfahren zum Beizen tierischer Bloessen
DE1203416B (de) * 1956-04-14 1965-10-21 Roehm & Haas Gmbh Verfahren zur Herstellung tierischer Bloessen
DE1211349B (de) * 1959-03-26 1966-02-24 Roehm & Haas Gmbh Enzymatische Enthaarung mit Pankreastryptase
DE1219620B (de) * 1953-09-04 1966-06-23 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE1230169B (de) * 1962-04-06 1966-12-08 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE1282837B (fi) * 1963-05-09 1968-11-14
DE1282838B (de) * 1964-01-22 1968-11-14 Roehm & Haas Gmbh Verfahren zum Weichen, Enthaaren oder Beizen von Fellen oder Haeuten mit proteolytischen Enzymen
DE1288728B (de) * 1963-07-27 1969-02-06 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
US3549495A (en) * 1967-02-17 1970-12-22 Roehm & Haas Gmbh Process for loosening the fiber structure of tanned furs
US3557002A (en) * 1967-11-15 1971-01-19 Procter & Gamble Stabilized aqueous enzyme preparation
US3558430A (en) * 1967-03-03 1971-01-26 Roehm & Haas Gmbh Process for the loosening of dead hairs in fur pelts
US3623950A (en) * 1968-04-13 1971-11-30 Roehm Gmbh Enzymatic dehairing process
US3741902A (en) * 1971-05-24 1973-06-26 Purex Corp Laundry prespotter composition
US3781212A (en) * 1972-10-27 1973-12-25 Townsend & Townsend Aerosol enzyme detergents stabilized with carbon dioxide
US3939040A (en) * 1973-04-28 1976-02-17 Rohm Gmbh Enzymatic bating method
US3966551A (en) * 1974-02-01 1976-06-29 Rohm Gmbh Method for preparing tannable pelts from animal skins and hides
US3986926A (en) * 1973-01-13 1976-10-19 Rohm Gmbh Method for preparing tannable pelts from animal skins and hides
CH631486A5 (en) * 1977-02-11 1982-08-13 Freudenberg Carl Process for working up hide wastes
DE3312840A1 (de) * 1983-04-09 1984-10-11 Röhm GmbH, 6100 Darmstadt Verfahren zur nassentfettung von hautmaterial
US4636222A (en) * 1984-08-07 1987-01-13 Rohm Gmbh Enzymatic unhairing method

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3600319A (en) * 1968-06-25 1971-08-17 Procter & Gamble Process for application of enzymes to spray-dried detergent granules
US3746649A (en) * 1971-10-01 1973-07-17 J Barrett Stable liquid enzyme product
DE2536256C3 (de) * 1975-08-14 1979-08-30 Bergmann, Christian, 2061 Nahe Der Abstützung der Propellerwelle eines Schiffes dienende Stevenlagerung
IT1151796B (it) * 1982-06-09 1986-12-24 Ravizza Spa Shampoo a base enzimatica
US4529525A (en) * 1982-08-30 1985-07-16 Colgate-Palmolive Co. Stabilized enzyme-containing detergent compositions
US4519934A (en) * 1983-04-19 1985-05-28 Novo Industri A/S Liquid enzyme concentrates containing alpha-amylase
DE3440750A1 (de) * 1984-11-08 1986-05-07 Röhm GmbH, 6100 Darmstadt Verfahren zum hautaufschluss von grossviehhaeuten und kalbfellen
US4753750A (en) * 1984-12-31 1988-06-28 Delaware Liquid laundry detergent composition and method of use
DE3513253C2 (de) * 1985-04-13 1997-04-10 Roehm Gmbh Verfahren zur raschen enzymatischen Enthaarung von Häuten
US4673647A (en) * 1985-05-06 1987-06-16 Miles Laboratories, Inc. Process to solubilize enzymes and an enzyme liquid product produced thereby
SE468518B (sv) * 1985-07-26 1993-02-01 Colgate Palmolive Co Stabiliserad textilmjukgoerande enzyminnehaallande foerstaerkt flytande detergentkomposition och dess anvaendning vid tvaett av textilier
NZ216791A (en) * 1985-07-26 1988-07-28 Colgate Palmolive Co Stabilised, built, enzyme-containing liquid detergents

Patent Citations (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE200519C (fi) * 1907-06-06
DE288095C (de) * 1914-11-11 1915-10-18 Roehm Otto Verfahren zum Weichen von Häuten und Fellen
DE847947C (de) * 1943-09-11 1952-08-28 Roehm & Haas G M B H Beizverfahren fuer Pelzfelle
DE1219620B (de) * 1953-09-04 1966-06-23 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE927464C (de) * 1953-09-04 1955-05-09 Roehm & Haas G M B H Verfahren zur Herstellung gerbfertiger Bloessen
DE976602C (de) * 1954-02-16 1964-01-02 Roehm & Haas G M B H Weichverfahren fuer rohe tierische Felle und Haeute
DE941680C (de) * 1954-04-17 1956-04-19 Roehm & Haas G M B H Verfahren zur Vorbehandlung von geweichten Pelzfellen fuer die Gerbung
DE976107C (de) * 1954-05-19 1963-02-28 Roehm & Haas G M B H Verfahren zum Beizen tierischer Hautbloessen fuer Chevreauleder
DE1023183B (de) * 1954-06-30 1958-01-23 Roehm & Haas Gmbh Verfahren zum AEschern von Fellen und Haeuten mit Hilfe von Schimmelpilztryptase
DE941811C (de) * 1954-11-18 1956-04-19 Roehm & Haas G M B H Verfahren zur Herstellung gerbfertiger Bloessen
DE974813C (de) * 1954-12-24 1961-05-04 Roehm & Haas G M B H Verfahren zum Beizen tierischer Hautbloessen
DE975095C (de) * 1955-01-01 1961-08-10 Roehm & Haas G M B H Verfahren zum Beizen tierischer Bloessen mit Pankreasenzympraeparaten
DE976928C (de) * 1955-01-08 1964-08-20 Roehm & Haas G M B H Verfahren zum Beizen tierischer Bloessen
DE1120066B (de) * 1955-03-23 1961-12-21 Roehm & Haas Gmbh Verfahren zum Beizen tierischer Hautbloessen
DE1134474B (de) * 1955-03-30 1962-08-09 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE1026038B (de) * 1955-03-30 1958-03-13 Roehm & Haas Gmbh Enthaaren und Entwollen gruener oder geweichter Felle
DE1034317B (de) * 1955-05-27 1958-07-17 Roehm & Haas Gmbh Verfahren zum Weichen von Rohhaeuten und -fellen
DE1022748B (de) * 1955-11-30 1958-01-16 Roehm & Haas Gmbh Weichen von Fellen und Haeuten
DE1203416B (de) * 1956-04-14 1965-10-21 Roehm & Haas Gmbh Verfahren zur Herstellung tierischer Bloessen
DE1211349B (de) * 1959-03-26 1966-02-24 Roehm & Haas Gmbh Enzymatische Enthaarung mit Pankreastryptase
DE1155560B (de) * 1960-06-04 1963-10-10 Roehm & Haas Gmbh Enthaaren von Haeuten und Fellen mit Hilfe proteolytischer Enzyme
DE1230169B (de) * 1962-04-06 1966-12-08 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE1282837B (fi) * 1963-05-09 1968-11-14
DE1288728B (de) * 1963-07-27 1969-02-06 Roehm & Haas Gmbh Verfahren zur Herstellung gerbfertiger Bloessen
DE1282838B (de) * 1964-01-22 1968-11-14 Roehm & Haas Gmbh Verfahren zum Weichen, Enthaaren oder Beizen von Fellen oder Haeuten mit proteolytischen Enzymen
US3549495A (en) * 1967-02-17 1970-12-22 Roehm & Haas Gmbh Process for loosening the fiber structure of tanned furs
US3558430A (en) * 1967-03-03 1971-01-26 Roehm & Haas Gmbh Process for the loosening of dead hairs in fur pelts
US3557002A (en) * 1967-11-15 1971-01-19 Procter & Gamble Stabilized aqueous enzyme preparation
US3623950A (en) * 1968-04-13 1971-11-30 Roehm Gmbh Enzymatic dehairing process
US3741902A (en) * 1971-05-24 1973-06-26 Purex Corp Laundry prespotter composition
US3781212A (en) * 1972-10-27 1973-12-25 Townsend & Townsend Aerosol enzyme detergents stabilized with carbon dioxide
US3986926A (en) * 1973-01-13 1976-10-19 Rohm Gmbh Method for preparing tannable pelts from animal skins and hides
US3939040A (en) * 1973-04-28 1976-02-17 Rohm Gmbh Enzymatic bating method
US3966551A (en) * 1974-02-01 1976-06-29 Rohm Gmbh Method for preparing tannable pelts from animal skins and hides
CH631486A5 (en) * 1977-02-11 1982-08-13 Freudenberg Carl Process for working up hide wastes
DE3312840A1 (de) * 1983-04-09 1984-10-11 Röhm GmbH, 6100 Darmstadt Verfahren zur nassentfettung von hautmaterial
US4636222A (en) * 1984-08-07 1987-01-13 Rohm Gmbh Enzymatic unhairing method

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
Kazandjian et al., "Enzymatic Analysis in Organic Solvents" Biotechnology and Bioengineering vol. XXVIII pp. 417-21 (1986).
Kazandjian et al., Enzymatic Analysis in Organic Solvents Biotechnology and Bioengineering vol. XXVIII pp. 417 21 (1986). *
Zaks, et al., "Enzyme-catalyzed process in organic solvents" Proc. Natl. Acad. Science USA vol. 82, pp. 3192-96. May (1985).
Zaks, et al., Enzyme catalyzed process in organic solvents Proc. Natl. Acad. Science USA vol. 82, pp. 3192 96. May (1985). *

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5531795A (en) * 1992-12-10 1996-07-02 Novo Nordisk A/S Method for casein finishing of leather
US5710040A (en) * 1995-02-24 1998-01-20 Roehm Gmbh Chemische Fabrik Stable enzymatic aqueous liquid composition for the production of leather
AU697192B2 (en) * 1995-02-24 1998-10-01 Rohm Gmbh Enzyme preparations for use in leather processing
AU2003217445B2 (en) * 2002-07-15 2008-10-02 Council Of Scientific And Industrial Research Total lime and sulfide free unhairing process using animal and/or plant enzymes
US20040006825A1 (en) * 2002-07-15 2004-01-15 Chellan Rose Process for lime and sulfide free unhairing of skins or hides using animal and/or plant enzymes
WO2004007774A1 (en) * 2002-07-15 2004-01-22 Council Of Scientific And Industrial Research Total lime and sulfide free unhairing process using animal and/or plant enzymes
CN100523219C (zh) * 2002-07-15 2009-08-05 科学与工业研究会 使用动物和/或植物酶但完全不用石灰和硫化物的去毛方法
AU2003217445C1 (en) * 2002-07-15 2009-02-26 Council Of Scientific And Industrial Research Total lime and sulfide free unhairing process using animal and/or plant enzymes
US7198647B2 (en) 2002-07-15 2007-04-03 Council Of Scientific And Industrial Research Process for lime and sulfide free unhairing of skins or hides using animal and/or plant enzymes
US7771489B2 (en) * 2002-08-14 2010-08-10 Basf Aktiengesellschaft Formulation for use in chrome or chrome-free tannage
US20060101584A1 (en) * 2002-08-14 2006-05-18 Basf Aktiengesellschaft Formulation for use in chrome or chrome-free tannage
US6827041B2 (en) 2002-12-20 2004-12-07 Frank Jay Hague Bleached expanded pigskin and products
US7013838B2 (en) 2002-12-20 2006-03-21 Frank Jay Hague Bleached expanded pigskin and products
US20050071927A1 (en) * 2002-12-20 2005-04-07 Vision International, L.L.C. Bleached expanded pigskin and products
US20040118360A1 (en) * 2002-12-20 2004-06-24 Visional International, L.L.C. Bleached expanded pigskin and products
US20120142073A1 (en) * 2010-08-05 2012-06-07 West Bengal University Of Technology Hide processing methods and compositions
US8524481B2 (en) * 2010-08-05 2013-09-03 West Bengal University Of Technology Hide processing methods and compositions
US20120097889A1 (en) * 2010-10-26 2012-04-26 Novozymes Biologicals, Inc. Wastewater Treatment Compositions
AU2011320630B2 (en) * 2010-10-26 2015-05-14 Novozymes Biologicals, Inc. Wastewater treatment compositions
US9988292B2 (en) * 2010-10-26 2018-06-05 Novozymes Biologicals, Inc. Wastewater treatment compositions
US10501336B2 (en) 2013-12-04 2019-12-10 Zhuangdou Zhang Tannery process with effluent recycling
US11040890B2 (en) 2013-12-04 2021-06-22 Zhuangdou Zhang Tannery process with effluent recycling
RU2588984C2 (ru) * 2014-07-04 2016-07-10 Михаил Вячеславович Новиков Способ выделки меховых шкурок
US20160186275A1 (en) * 2014-12-22 2016-06-30 Zhuangdou Zhang Tanning Process With Reduced Waste Discharge

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AU1165688A (en) 1988-08-18
GB2201960B (en) 1990-11-21
WO1988006183A1 (en) 1988-08-25
SE500913C2 (sv) 1994-09-26
FI93656C (fi) 1995-05-10
DK73688A (da) 1988-08-14
SE8800238L (sv) 1988-08-14
GB8803314D0 (en) 1988-03-09
FI93656B (fi) 1995-01-31
DE3704465A1 (de) 1988-08-25
BR8805403A (pt) 1989-08-15
JP2703250B2 (ja) 1998-01-26
FR2610947B1 (fr) 1989-12-08
IT8867104A0 (it) 1988-02-12
FR2610947A1 (fr) 1988-08-19
FI884592A0 (fi) 1988-10-06
DK73688D0 (da) 1988-02-12
IT1219015B (it) 1990-04-24
GB2201960A (en) 1988-09-14
ES2008974A6 (es) 1989-08-16
FI884592A (fi) 1988-10-06
DE3704465C2 (de) 1995-11-02
AU618523B2 (en) 1992-01-02
US4943530A (en) 1990-07-24
KR960016075B1 (ko) 1996-11-27
CH677798A5 (fi) 1991-06-28
SE8800238D0 (sv) 1988-01-26
JPS63216480A (ja) 1988-09-08
KR880010113A (ko) 1988-10-07

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